Scrubber with multiple venturis

ABSTRACT

A scrubber removes matter (e.g., particulate, gaseous, or liquid) from a gas stream in order to recover the matter and/or to clean the gas. In particular aspects, the scrubber contains multiple venturis that may provide additional flexibility and increased efficiency. The invention also pertains to related methods.

RELATED APPLICATION

This application claims the benefit of priority to U.S. App. No.61/019,695 filed on Jan. 8, 2008.

BACKGROUND OF THE INVENTION

In some aspects, this invention generally relates to scrubbers used toremove matter (e.g., particulate, gaseous, or liquid) from a gas streamin order to recover the matter and/or to clean the gas. In particularaspects, this invention relates to a positioning of multiple venturisthat may provide additional flexibility and increased efficiency. Theinvention also pertains to related methods.

Scrubbers—such as those described in U.S. Pat. Nos. 5,279,646;5,484,471; 5,512,085; and 5,759,233—are known. FIG. 1 of U.S. Pat. No.5,512,085, for example, shows an example of extant technology.

This system of the '085 patent is quite simple. Gas enters the venturiportion of the scrubber (on the left) where a liquid is sprayed in tothe throat of the venturi. In many instances, the diameter of theventuri throat can be approximately 12″ to 48″.

The purpose of the venturi is to impact the liquid with the matter to beremoved. The liquid is then separated from the gas through impact with aliquid level at the bottom of the venturi, and through centrifugalforces in the separator vessel (on the right). There can be a demisterat the top of the separator vessel, or external to the separator vessel,to remove any residual liquid droplets.

An advantage of this technology is that it can be very inexpensive. Adisadvantage is that it may not be efficient enough to meet gascleanliness standards set by regulatory agencies. Another disadvantageis that a high pressure drop across the venturi may be required toachieve high efficiency, which costs the mill energy and possiblyequipment upgrades.

Other scrubbers are also known. For example, FIG. 1 shows a scrubberthat is quite different than the ones mentioned above.

In FIG. 1, the inlet 10 is not a venturi, but rather a duct with spraynozzle(s) 12 used to quench the gases to saturation. In this illustrateddevice, there are multiple venturis 30 positioned within the separatorvessel 20, each with its own spray nozzle 32. These venturis may havethroats with a diameter of between 6″ and 12″. In a preferredembodiment, the venturi may have a throat of approximately 8″. There maybe a preliminary cleaning step (shown by sprayer 42) and demister(s) 40,as shown in this figure.

An advantage of this system is that it may be highly efficient at a lowpressure drop. A disadvantage is that it may be very expensive relativeto a system with an external venturi. Another disadvantage is that itmay require modification to an existing (e.g., older) vessel in the caseof a retrofit project.

In light of the above-identified deficiencies of the prior art, thereexists a need for an improved scrubber, particularly a scrubber thatenables a good efficiency and reasonable pressure drop.

In certain embodiments, the multiple venturis of the present inventionmay provide flexibility in scaling up and scaling down the separationprocess, thus enabling a wider range of operating parameters, processconditions, and loading. The multiple venturis may also facilitaterepairs, as each venturi unit may be replaced, repaired, orreconstructed individually. This flexibility may not only reducedowntime, but may also provide flexibility in designing, testing, andevaluating new configurations and devices. Furthermore, at least certainembodiments of the present invention are particularly suitable forrelatively inexpensive retrofits to existing equipment.

BRIEF DESCRIPTION OF THE INVENTION

In an embodiment, the present invention generally relates to a systemfor removing matter from a gaseous stream. The matter may comprisesolids, liquids, or gasses. The system for the separation of matter froma gaseous stream may include: a cyclonic separator vessel adapted toreceive a first outlet stream and a second outlet stream; and a firstventuri external to the cyclonic separator vessel and a second venturiexternal to the cyclonic separator vessel. The first and second venturismay be arranged in parallel and each adapted to receive a portion of aninlet stream comprising gas and matter to be separated from the gas. Thefirst and second venturis may further be each adapted to receive anddistribute a solvent to entrain the matter to be separated from the gas.The first venturi may be adapted to discharge the first outlet stream,and the second venturi may be adapted to discharge the second outletstream. The first and second outlet steams each include gas andentrained matter to be separated from the gas. The cyclonic separatorvessel may be adapted to separate the entrained matter from the gas.

In another embodiment, the present invention relates to a method ofseparating matter from a gaseous stream. The method may comprise:providing a gaseous stream comprising solid, liquid, or gaseous matterto be removed from the stream; dividing the gaseous stream into two ormore gaseous streams; providing at least two venturis, wherein the atleast two venturis each comprise a nozzle, an inlet cone, a throat, andan outlet cone; feeding each of the divided streams into one of the atleast two venturis; mixing a solvent from the nozzle in at least one ofthe at least two venturis with the divided stream so as to entrain thematter and facilitate separation in a separator; providing the separatordownstream of the at least two venturis; connecting the separator to theat least two venturis; and separating the entrained matter from thegaseous stream in the separator.

In some embodiments, the venturis are identical or may be of differentsizes.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a prior art scrubber.

FIG. 2 illustrates a scrubber in accordance with an exemplary embodimentof the present invention.

DETAILED DESCRIPTION OF THE INVENTION

There are three main scrubber applications used in the processing ofpulp and paper: kiln, power boiler, and dissolving tank scrubbers. Asidefrom those primary uses, there are secondary, more minor applicationsfor scrubbers. In various embodiments, this invention relates to primaryand secondary scrubber applications. More specifically, this inventionmay be used in connection with scrubbers intended to remove matter(e.g., particulate, gaseous, or liquid) from a gas stream in order torecover the matter and/or to clean the gas. In one aspect, the scrubberdescribed herein may have particular utility in remediating a gaseousstream containing pollution prior to exhausting to the atmosphere.

In one embodiment, there is a system including multiple venturis (e.g.,four venturis) external to the separator vessel. The gaseous streamcontaining the matter to be separated (e.g., particulate, gaseous, orliquid matter) may be split across the multiple venturis. As is wellunderstood in the art, a venturi generally includes a gaseous streambeing contacted with a liquid emitted from a high pressure spray nozzle.The injected liquid may form droplets that scrub the to-be-separatedmatter in the gaseous stream. That is, a high pressure spray passingthrough the venturi throat may form numerous fine liquid droplets thatprovide turbulent mixing between the gas and liquid phases. A venturigenerally has a changing cross-sectional area, which generally decreasesthen increases. These and other configurations are contemplated withinvarious embodiments of the present invention.

In a preferred embodiment, these venturis would be arranged in parallel,although a series of multiple venturis are also contemplated in otherembodiments. Indeed, the multiple venturis may be combined a virtuallylimitless number of permutations involving venturis in parallel andseries.

The multiple venturis thus may provide flexibility in scaling up andscaling down the separation process, thus enabling a wider range ofoperating parameters, process conditions, and loading. The multipleventuris may also facilitate repairs, as each venturi unit may bereplaced, repaired, or reconstructed individually. This flexibility maynot only reduce downtime, but may also provide flexibility in designing,testing, and evaluating new configurations and devices. Furthermore, atleast certain embodiments of the present invention are particularlysuitable for relatively inexpensive retrofits to existing equipment.

In a preferred embodiment involving multiple venturis solely inparallel, each venturi would be responsible for handling a fraction ofthe incoming gaseous stream containing the matter to be separated. Insuch an arrangement, the diameter of each venturi may be, for example,approximately 12″. In comparison to a single venturi, there may not be adirect correlation between the fraction of incoming gaseous stream anddiameter. That is, the diameter or cross-sectional area of each venturimay depend on a number of different factors, including, for example,angles of the venturi's inlet and outlet cones, length of the venturi'sthroat, pressure drop, etc.

A preferred embodiment is schematically illustrated in FIG. 2. Thisembodiment illustrates four venturis in parallel, though otherpermutations involving greater and fewer venturis as well as venturi(s)in series are also contemplated. For example, certain embodiments of thepresent invention may include two, three, four, five, six, seven, eight,nine, ten, or more venturis, solely in parallel or in parallel and inseries.

FIG. 2 illustrates an overall air pollution control system includingmultiple venturis and a separator. A contaminant-laden gaseous stream isgenerated by a source (not shown). This source may be involved in pulpand paper-making, such as, for example, a kiln. The gaseous stream mayhave liquid, solid, or gaseous matter entrained therein, includinggaseous contaminants that may condense as the gaseous stream is cooled(if heated).

The gaseous stream enters via conduit 202, which is split (either evenlyor unevenly) among four streams into conduits 204. Although the divisionis depicted as a series (i.e., with a fraction of conduit 202 beingsectioned off at each conduit 204), it is possible to use otherarrangements, such as a parallel division into four streams at asingular node. If heated, the gaseous stream may be cooled to a lowertemperature in forechambers 214 prior to entering venturis 210. Thiscooling may occur with water or other liquid(s) emitted from nozzles206. This cooling may lower the temperature of the gaseous stream toapproximately the saturation temperature.

The nozzles 206 may be positioned remotely from the entrance to thethroats 212 of the venturis. After flowing through forechambers 214, theeffluent enters the venturi scrubbers 210 comprising entrance cones 216,throats 212 and an exit cone 218. The scrubbing liquid for the venturiis provided by the spray from nozzles 208. In some instances, nozzles208 may be two-fluid nozzles which form a spray of scrubbing liquidhaving droplets which are optimized for maximum collection of opticallyactive particles. In some embodiments, nozzles 208 may be connected to asource of water or other solvent and a source of compressed air.

The entrance or inlet cones 216 may have a wide range of angles. In someembodiments, the angle of the inlet cone may be between 60° and 90°, andin other embodiments, the angle of the inlet cone may be between 30° and45° or between 45° and 60°. A relatively larger angle may require anincrease in energy required to move gas through the venturi, though itmay also improve scrubbing efficiency by maximizing the differentialvelocity between the contaminant particles and the scrubbing droplets.

The outlet cones 218 may be relatively long, which may maximize therecovery of energy from both the gas flow and from the droplets.Scrubbing may also occur in the outlet cone as the scrubbing dropletsand any remaining contaminant particles decelerate at different rates.The precise configuration of the venturis, including the angles of theinlet cones and outlet cones, and the cross-sectional area may varyaccording to different embodiments of the present invention. Anysuitable configuration of venturi(s) may be used.

The spray from nozzles 206 may introduce the scrubbing liquid relativelyuniformly into the gaseous stream, such that cooling is uniformlyachieved and the gas flow and the scrubbing liquid form an homogenousmixture when they enter the venturis 210. In some embodiments, thedifferential velocity between the spray droplets and the gas flow at thepoint of introduction is low. Depending on the embodiments, the spraymay or may not assist the flow of gases through the venturis.

It should be appreciated that the venturis 210 need not be identical,and that different sized venturis may be used. In such an embodiment,each venturi may be designed to handle a different flowrate and/orcomposition of the gaseous stream. In this respect, furthermore,individual venturis may be brought online as necessary according tovarying process conditions and/or loading. In yet further embodiments,there may be greater than or less than four venturis in series and/orparallel.

After leaving the exit cones 218 of the venturis 210, the contaminantladen spray droplets are removed from the effluent stream. In theexemplary system depicted in FIG. 2, a cyclonic separator 220 and a misteliminator 234 and nozzles 222 may be used to remove the contaminatedspray droplets from the effluent gas flow. Sprays from a plurality ofnozzles 222 may be introduced into the gas flow just upstream of themist eliminator 234 to keep the surface of the mist eliminator wet andclean. The operation of cyclonic separators and of mist eliminators arewell known to those skilled in the art and any suitable configurationmay be used in connection with the invention described herein. Becausethe mixture of the gaseous stream and spray droplets may have beenreduced to substantially saturation temperature, there may be little orno evaporation of the scrubbing droplets after they exit the venturis.

As depicted in FIG. 2, streams exit from each venturi 210 and connect tocyclonic separator 220 via conduit 230. Stream 232 exits from separator220 and may be further cleaned and/or recycled to various processes, inaccordance with various embodiments.

While the invention has been described in connection with what ispresently considered to be the most practical and preferred embodiment,it is to be understood that the invention is not to be limited to thedisclosed embodiment, but on the contrary, is intended to cover variousmodifications and equivalent arrangements included within the spirit andscope of the appended claims.

1. A system for the separation of matter from a gaseous streamcomprising: a cyclonic separator vessel adapted to receive a firstoutlet stream and a second outlet stream; and a first venturi externalto the cyclonic separator vessel and a second venturi external to thecyclonic separator vessel, wherein the first and second venturis arearranged in parallel and each are adapted to receive a portion of aninlet stream comprising gas and matter to be separated from the gas andeach are adapted to receive and distribute a solvent to entrain thematter to be separated from the gas and wherein the first venturi isadapted to discharge the first outlet stream and the second venturi isadapted to discharge the second outlet stream, wherein the first andsecond outlet steams each include gas and entrained matter to beseparated from the gas; wherein the cyclonic separator vessel is adaptedto separate the entrained matter from the gas.
 2. The system of claim 1,wherein the matter to be separated from the gas comprises solid, liquid,or gaseous matter.
 3. The system of claim 1, wherein the matter to beseparated from the gas comprises solid matter generated in a processrelating to pulp and paper-making.
 4. The system of claim 1, wherein thefirst venturi and the second venturi each comprise a nozzle, an inletcone, a throat, and an outlet cone.
 5. The system of claim 4, whereinthe throat of the first or second venturi has a diameter of between 6inches and 12 inches.
 6. The system of claim 4, wherein the inlet coneof the first or second venturi has an angle between 60° and 90°.
 7. Thesystem of claim 4, wherein the inlet cone of the first or second venturihas an angle between 30° and 45°.
 8. The system of claim 4, wherein theinlet cone of the first or second venturi has an angle between 45° and60°.
 9. The system of claim 1, wherein the solvent is water.
 10. Thesystem of claim 1, further comprising a third venturi external to thecyclonic separator vessel, wherein the third venturi is arranged inparallel with the first and second venturis and is adapted to receive aportion of an inlet stream comprising gas and matter to be separatedfrom the gas and is adapted to receive and distribute a solvent toentrain the matter to be separated from the gas and wherein the thirdventuri is adapted to discharge a third outlet stream, wherein the thirdoutlet steam includes gas and entrained matter to be separated from thegas and wherein the cyclonic separator vessel is adapted to receive thethird outlet stream.
 11. The system of claim 10, further comprising afourth venturi external to the cyclonic separator vessel, wherein thefourth venturi is arranged in parallel with the first, second, and thirdventuris and is adapted to receive a portion of an inlet streamcomprising gas and matter to be separated from the gas and is adapted toreceive and distribute a solvent to entrain the matter to be separatedfrom the gas and wherein the fourth venturi is adapted to discharge afourth outlet stream, wherein the fourth outlet steam includes gas andentrained matter to be separated from the gas and wherein the cyclonicseparator vessel is adapted to receive the fourth outlet stream.
 12. Thesystem of claim 1, wherein the cyclonic separator vessel is adapted toreceive a combined stream comprising the first outlet stream and thesecond outlet stream.
 13. The system of claim 1, wherein the inletstream is divided unevenly between the first venturi and the secondventuri such that the first venturi and the second venturis havedifferent sizing according to the different flowrates of the gaseousinlet stream.
 14. The system of claim 1, wherein the entire inlet streamis directed to the first venturi.
 15. A method of separating matter froma gaseous stream, the method comprising: providing a gaseous streamcomprising solid, liquid, or gaseous matter to be removed from thestream; dividing the gaseous stream into two or more gaseous streams;providing at least two venturis, wherein the at least two venturis eachcomprise a nozzle, an inlet cone, a throat, and an outlet cone; feedingeach of the divided streams into one of the at least two venturis;mixing a solvent from the nozzle in at least one of the at least twoventuris with the divided stream so as to entrain the matter andfacilitate separation in a separator; providing the separator downstreamof the at least two venturis; connecting the separator to the at leasttwo venturis; and separating the entrained matter from the gaseousstream in the separator.
 16. The method of claim 15, wherein the step ofmixing the solvent from the nozzle in at least one of the at least twoventuris with the divided stream so as to entrain the matter andfacilitate separation in a separator comprises spraying the solventunder high pressure such that turbulent mixing occurs between gas andliquid phases in the venturi.
 17. The method of claim 15, wherein thesolvent comprises water.
 18. The method of claim 15, wherein the step ofseparating the entrained matter from the gaseous stream in the separatorcomprises inducing a cyclone in the separator.
 19. The method of claim15 further providing at least three venturis, wherein the at least threeventuris each comprise a nozzle, an inlet cone, a throat, and an outletcone.
 20. The method of claim 15, wherein the matter to be removed fromthe gaseous stream comprises particulate matter generated during pulp orpaper-making.